CN205825084U - A kind of My heat recovery - Google Patents

A kind of My heat recovery Download PDF

Info

Publication number
CN205825084U
CN205825084U CN201620725004.0U CN201620725004U CN205825084U CN 205825084 U CN205825084 U CN 205825084U CN 201620725004 U CN201620725004 U CN 201620725004U CN 205825084 U CN205825084 U CN 205825084U
Authority
CN
China
Prior art keywords
heat
chamber
dividing plate
heat recovery
smoke chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201620725004.0U
Other languages
Chinese (zh)
Inventor
黄冬良
陈件明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beijing Zhongcheng Yongyuan Energy Saving Environmental Protection Technology Co Ltd
Original Assignee
Beijing Zhongcheng Yongyuan Energy Saving Environmental Protection Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Beijing Zhongcheng Yongyuan Energy Saving Environmental Protection Technology Co Ltd filed Critical Beijing Zhongcheng Yongyuan Energy Saving Environmental Protection Technology Co Ltd
Priority to CN201620725004.0U priority Critical patent/CN205825084U/en
Application granted granted Critical
Publication of CN205825084U publication Critical patent/CN205825084U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/30Technologies for a more efficient combustion or heat usage

Abstract

This utility model relates to a kind of My heat recovery, the body formed including smoke chamber and heat-exchanging chamber, described smoke chamber is arranged on below described heat-exchanging chamber, described smoke chamber is respectively arranged on the left side and the right side gas approach and exhanst gas outlet, dividing plate it is provided with between smoke chamber and heat-exchanging chamber, described dividing plate is provided with the heat exchanger tube running through described dividing plate, described heat exchanger tube includes the base tube of cylinder, described base tube is positioned on the exterior periphery direction above described dividing plate and is provided with multiple first helical fin, described base tube is positioned on the exterior periphery direction below described dividing plate and is provided with multiple second helical fin, it is provided with sewage draining exit bottom described smoke chamber.The beneficial effects of the utility model are, it is provided that a kind of simple in construction, the My heat recovery that easy to use and waste heat recovery efficiency is high.

Description

A kind of My heat recovery
Technical field
This utility model relates to a kind of My heat recovery.
Background technology
Boiler is a kind of energy conversion, and the energy to boiler input has the chemical energy in fuel, electric energy, high-temperature flue gas The form such as heat energy, and change through boiler, outwards output has the steam of certain heat energy, high-temperature water or organic heat carrier.Make With the boiler of fuel when in use, the flue gas of generation is mostly discharged by chimney, but, flue gas is directly discharged from chimney Time, substantial amounts of heat energy discharges the most therewith, is also to cause one of reason that boiler efficiency is the highest;The flue gas being expelled directly out from chimney is also Substantial amounts of solid particle can be carried to environment.
Utility model content
In view of the above-mentioned problems in the prior art, main purpose of the present utility model is to solve lacking of prior art Fall into, the My heat recovery that this utility model provides a kind of simple in construction, easy to use and waste heat recovery efficiency is high.
This utility model provides a kind of My heat recovery, the basis formed including smoke chamber and heat-exchanging chamber Body, described smoke chamber is arranged on below described heat-exchanging chamber, and described smoke chamber is respectively arranged on the left side and the right side gas approach and flue gas Outlet, is provided with dividing plate between smoke chamber and heat-exchanging chamber, described dividing plate is provided with the heat exchanger tube running through described dividing plate, described heat exchange Pipe includes the base tube of cylinder, and described base tube is positioned on the exterior periphery direction above described dividing plate and is provided with multiple first spiral Fin, described base tube is positioned on the exterior periphery direction below described dividing plate and is provided with multiple second helical fin, described flue gas Sewage draining exit it is provided with bottom room.
Optionally, described base tube includes:
The housing sealed, described housing cylindrically shaped;
It is covered in the capillary structure of inner walls, in it, forms the liquid refrigerant flow channel for liquid Working fluid flow;
Being arranged in one layer of clad of capillary structure inwall, it is internally formed for the gaseous working medium for gaseous state Working fluid flow Flow channel;
Wherein, the lower end of described housing is used for being placed in smoke chamber to form evaporator section, and the upper end of described housing is used for It is placed in heat-exchanging chamber to form condensation segment;
Wherein, the gaseous working medium formed after described evaporator section evaporation process flows along described gaseous working medium flow channel Carrying out condensation process to described condensation segment, the liquid refrigerant formed after condensation is back to institute along described liquid refrigerant flow channel State evaporator section.
Optionally, the described heat-exchanging chamber left and right sides is respectively arranged with air outlet slit and air intlet.
Optionally, corner, described heat-exchanging chamber top is respectively arranged with a hanger.
Optionally, described smoke chamber inner bottom part is vertically arranged with multiple first gear aerofoil.
Optionally, described heat-exchanging chamber inner top is vertically arranged with multiple second gear aerofoil.
This utility model has the following advantages and beneficial effect:
1) My heat recovery provided by the utility model, with fuel boiler with the use of, allow use fuel The flue gas produced during boiler by gas approach, smoke chamber and exhanst gas outlet, flue gas in smoke chamber, flue gas substantial amounts of Heat energy exchange heat pipes heat, is then communicated in heat-exchanging chamber, can be entered the water in heat-exchanging chamber or air by heating plate Row heating.The sectional area of this utility model smoke chamber is more than the sectional area of gas approach, when flue gas enters cigarette by gas approach During air chamber, the flowing velocity of flue gas can reduce, and makes some solid granulates sink at smoke chamber, is no longer exhausted directly in air; This utility model has the good effect of the discharge of recovery section heat energy and minimizing solid particle;
2) heat exchanger tube of the present utility model is at capillary structure inner wall arrangement clad, and by clad by liquid refrigerant stream Dynamic passage and gaseous state Working fluid flow passage are isolated, so that gaseous state, liquid refrigerant will not produce convection current, and then reduce gas-liquid Convective resistance, simultaneously by multiple first helical fins being arranged on hull outside circumferencial direction and the second spiral aluminum fin-stock, Improve its radiating efficiency further;
3) clad of the present utility model is made up of the material that heat conductivility is good, therefore good heat conductivity, thus improves The heat transfer efficiency of heat exchanger tube;
4) simple in construction of heat exchanger tube of the present utility model, easy to use, and heat exchanger tube utilization rate is high, perfect heat-dissipating.
Accompanying drawing explanation
The structural representation of the My heat recovery that Fig. 1 provides for this utility model embodiment;
Fig. 2 is the structural representation of heat exchanger tube in Fig. 1;
Fig. 3 is the section view structure for amplifying schematic diagram of base tube in Fig. 2.
Detailed description of the invention
For making the purpose of this utility model embodiment, technical scheme and advantage clearer, new below in conjunction with this practicality Accompanying drawing in type embodiment, is clearly and completely described the technical scheme in this utility model embodiment, it is clear that retouched The embodiment stated is a part of embodiment of this utility model rather than whole embodiments.Generally described in the accompanying drawing herein and The assembly of this utility model embodiment illustrated can be arranged with various different configurations and design.Therefore, below to attached The detailed description of the embodiment of the present utility model provided in figure is not intended to limit claimed scope of the present utility model, But it is merely representative of selected embodiment of the present utility model.Based on the embodiment in this utility model, ordinary skill people The every other embodiment that member is obtained under not making creative work premise, broadly falls into the model of this utility model protection Enclose.
In description of the present utility model, " " center ", " on ", D score, "left", "right", " perpendicular it should be noted that term Directly ", " level ", " interior ", the orientation of the instruction such as " outward " or position relationship be based on orientation shown in the drawings or position relationship, be only Must have specific for the ease of describing this utility model and simplification description rather than instruction or the device of hint indication or element Orientation, with specific azimuth configuration and operation, therefore it is not intended that to restriction of the present utility model.Additionally, term " the One ", " second ", " the 3rd " are only used for describing purpose, and it is not intended that instruction or hint relative importance.
In description of the present utility model, in addition it is also necessary to explanation, unless otherwise clearly defined and limited, term " sets Put ", should be interpreted broadly " installation ", " being connected ", " connection ", connect for example, it may be fixing, it is also possible to be to removably connect, Or be integrally connected;Can be to be mechanically connected, it is also possible to be electrical connection;Can be to be joined directly together, it is also possible to pass through intermediary It is indirectly connected to, can be the connection of two element internals.For the ordinary skill in the art, can be according to concrete feelings Condition understands above-mentioned term concrete meaning in this utility model.
With specific embodiment, this utility model is further described below with reference to accompanying drawings.
As shown in Figures 1 to 3: a kind of My heat recovery of this utility model embodiment, including smoke chamber 100 He The body of heat-exchanging chamber 200 composition, smoke chamber 100 is arranged on below heat-exchanging chamber 200, and smoke chamber 100 left and right sides sets respectively There are gas approach 101 and exhanst gas outlet 102, are provided with dividing plate 503 between smoke chamber 100 and heat-exchanging chamber 200, dividing plate 503 sets Having the heat exchanger tube 500 running through dividing plate 700, heat exchanger tube 500 includes the base tube 501 of cylinder, and base tube 501 is positioned at above dividing plate 503 Exterior periphery direction on be provided with multiple first helical fin 502, base tube is positioned on the exterior periphery direction below dividing plate and sets It is equipped with multiple second helical fin 504, bottom smoke chamber, is provided with sewage draining exit 400.
As the preferred implementation of above-described embodiment, base tube 501 includes:
The housing 511 sealed, housing cylindrically shaped;
It is covered in the capillary structure 512 of inner walls, in it, forms the liquid refrigerant flow channel for liquid Working fluid flow;
Being arranged in one layer of clad 513 of capillary structure inwall, it is internally formed for the gaseous state for gaseous state Working fluid flow Working fluid flow passage;
Wherein, gaseous working medium flow channel interconnects with liquid refrigerant flow channel;
Wherein, the lower end of housing 511 is used for being placed in smoke chamber to form evaporator section, and the upper end of housing 511 is used for pacifying Put at heat-exchanging chamber to form condensation segment;
Wherein, the gaseous working medium formed after evaporator section evaporation process flow to condensation segment along gaseous working medium flow channel Carrying out condensation process, the liquid refrigerant formed after condensation is back to evaporator section along liquid refrigerant flow channel.
As the preferred implementation of above-described embodiment, heat-exchanging chamber 200 left and right sides is respectively arranged with air outlet slit 201 With air intlet 202.
As the preferred implementation of above-described embodiment, corner, heat-exchanging chamber 200 top is respectively arranged with a hanger 205, For lifting this My heat recovery.
As the preferred implementation of above-described embodiment, smoke chamber 100 inner bottom part is vertically arranged with multiple first gear aerofoil 600, for reducing flue gas velocity of liquid assets in this smoke chamber 100, flow through the flue-gas temperature of exhanst gas outlet with more preferable reduction.
As the preferred implementation of above-described embodiment, heat-exchanging chamber 200 inner top is vertically arranged with multiple second and keeps out the wind Plate 300, more preferably to heat the air in heat-exchanging chamber.
A kind of My heat recovery that this utility model embodiment provides, has the following advantages and beneficial effect:
1) My heat recovery provided by the utility model, with fuel boiler with the use of, allow use fuel The flue gas produced during boiler by gas approach, smoke chamber and exhanst gas outlet, flue gas in smoke chamber, flue gas substantial amounts of Heat energy exchange heat pipes heat, is then communicated in heat-exchanging chamber, can be entered the water in heat-exchanging chamber or air by heating plate Row heating;The sectional area of this utility model smoke chamber is more than the sectional area of gas approach, when flue gas enters cigarette by gas approach During air chamber, the flowing velocity of flue gas can reduce, and makes some solid granulates sink at smoke chamber, is no longer exhausted directly in air; This utility model has the good effect of the discharge of recovery section heat energy and minimizing solid particle;
2) heat exchanger tube of the present utility model is at capillary structure inner wall arrangement clad, and by clad by liquid refrigerant stream Dynamic passage and gaseous state Working fluid flow passage are isolated, so that gaseous state, liquid refrigerant will not produce convection current, and then reduce gas-liquid Convective resistance, simultaneously by multiple first helical fins being arranged on hull outside circumferencial direction and the second spiral aluminum fin-stock, Improve its radiating efficiency further;
3) clad of the present utility model is made up of the material that heat conductivility is good, therefore good heat conductivity, thus improves The heat transfer efficiency of heat exchanger tube;
4) simple in construction of heat exchanger tube of the present utility model, easy to use, and heat exchanger tube utilization rate is high, perfect heat-dissipating.
Last it is noted that above-described each embodiment is merely to illustrate the technical solution of the utility model, rather than It is limited;Although this utility model being described in detail with reference to previous embodiment, those of ordinary skill in the art It is understood that the technical scheme described in previous embodiment still can be modified by it, or to the most part or all of Technical characteristic carries out equivalent;And these amendments or replacement, do not make the essence of appropriate technical solution depart from this utility model The scope of each embodiment technical scheme.

Claims (6)

1. a My heat recovery, it is characterised in that include smoke chamber and the body of heat-exchanging chamber composition, described cigarette Air chamber is arranged on below described heat-exchanging chamber, and described smoke chamber is respectively arranged on the left side and the right side gas approach and exhanst gas outlet, flue gas Being provided with dividing plate between room and heat-exchanging chamber, described dividing plate is provided with the heat exchanger tube running through described dividing plate, and described heat exchanger tube includes circle The base tube of cylindricality, described base tube is positioned on the exterior periphery direction above described dividing plate and is provided with multiple first helical fin, institute State base tube to be positioned on the exterior periphery direction below described dividing plate and be provided with multiple second helical fin, set bottom described smoke chamber It is equipped with sewage draining exit.
My heat recovery the most according to claim 1, it is characterised in that described base tube includes:
The housing sealed, described housing cylindrically shaped;
It is covered in the capillary structure of inner walls, in it, forms the liquid refrigerant flow channel for liquid Working fluid flow;
Being arranged in one layer of clad of capillary structure inwall, it is internally formed for the gaseous working medium flowing for gaseous state Working fluid flow Passage;
Wherein, the lower end of described housing is used for being placed in smoke chamber to form evaporator section, and the upper end of described housing is used for disposing At heat-exchanging chamber to form condensation segment;
Wherein, the gaseous working medium formed after described evaporator section evaporation process flow to institute along described gaseous working medium flow channel Stating condensation segment and carry out condensation process, the liquid refrigerant formed after condensation is back to described steaming along described liquid refrigerant flow channel Send out section.
My heat recovery the most according to claim 1, it is characterised in that the described heat-exchanging chamber left and right sides is divided It is not provided with air outlet slit and air intlet.
My heat recovery the most according to claim 3, it is characterised in that corner, described heat-exchanging chamber top is divided It is not provided with a hanger.
My heat recovery the most according to claim 1, it is characterised in that described smoke chamber inner bottom part longitudinally sets It is equipped with multiple first gear aerofoil.
My heat recovery the most according to claim 1, it is characterised in that described heat-exchanging chamber inner top is longitudinally It is provided with multiple second gear aerofoil.
CN201620725004.0U 2016-07-11 2016-07-11 A kind of My heat recovery Expired - Fee Related CN205825084U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620725004.0U CN205825084U (en) 2016-07-11 2016-07-11 A kind of My heat recovery

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620725004.0U CN205825084U (en) 2016-07-11 2016-07-11 A kind of My heat recovery

Publications (1)

Publication Number Publication Date
CN205825084U true CN205825084U (en) 2016-12-21

Family

ID=57564454

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620725004.0U Expired - Fee Related CN205825084U (en) 2016-07-11 2016-07-11 A kind of My heat recovery

Country Status (1)

Country Link
CN (1) CN205825084U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109489460A (en) * 2018-11-27 2019-03-19 重庆大学 A kind of ash-laden gas stage purification residual neat recovering system and dedusting store heat-exchanger rig
CN109681896A (en) * 2018-12-25 2019-04-26 江苏理文造纸有限公司 A kind of boiler smoke thermal energy recycling device
CN110836612A (en) * 2018-08-16 2020-02-25 贺天欣 Domestic energy-saving hot-pipe water cooler

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110836612A (en) * 2018-08-16 2020-02-25 贺天欣 Domestic energy-saving hot-pipe water cooler
CN109489460A (en) * 2018-11-27 2019-03-19 重庆大学 A kind of ash-laden gas stage purification residual neat recovering system and dedusting store heat-exchanger rig
WO2020107826A1 (en) * 2018-11-27 2020-06-04 重庆大学 Staged purification and waste heat recovery system for dust-containing flue gas and dedusting heat storage and exchange device
CN109681896A (en) * 2018-12-25 2019-04-26 江苏理文造纸有限公司 A kind of boiler smoke thermal energy recycling device

Similar Documents

Publication Publication Date Title
US9097470B2 (en) Internal liquid separating hood-type condensation heat exchange tube
CN205825084U (en) A kind of My heat recovery
CN105737631A (en) Heat tube type water-saving device used for cross-flow cooling tower
CN109292858B (en) Fresh water collection system and seawater desalination system thereof
CN111306812B (en) Solar energy system, heat supply ventilation system and building roof thereof
CN111536818B (en) Heat storage heat exchanger and fresh air system for controlling PM2.5
CN110986239B (en) Ventilation system utilizing solar energy and building thereof
CN102384682A (en) Internal-circulation special high-efficiency heat exchanger
CN205825083U (en) A kind of flue gas waste heat recoverer
CN206192157U (en) Novel waste heat of boiler flue gas recoverer
CN113108490B (en) Solar energy new trend system
CN111981882B (en) Discontinuous phase separation loop heat pipe
CN204923933U (en) Evaporative condenser
CN103712495A (en) Heat exchange device for recycling flue gas waste heat
CN203100177U (en) Condensing heat exchanger
CN202254987U (en) Special high-efficiency heat exchanger
CN206291766U (en) A kind of heat exchanger tube
CN106152811A (en) A kind of High Efficiency Thermal gas condensing unit
CN206291767U (en) A kind of novel heat exchange pipe
CN206399249U (en) A kind of shell-and-tube heat exchanger
CN105466234A (en) Double-loop water-cooling flue gas condenser
CN206488665U (en) A kind of flue gas heat-exchange unit
CN111174618B (en) Heat storage heat exchanger and fresh air system
CN203224144U (en) Evaporator heat-radiating module of steam-turbine exhaust-steam residual-heat utilizing absorption-type heat pump
CN203642565U (en) Absorption refrigerator condenser based on heat tube bundle with enhanced condensing function

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20161221

Termination date: 20190711

CF01 Termination of patent right due to non-payment of annual fee